PROCESS FOR THE PREPARATION OF ETHYLENICALLY UNSATURATED COMPOUNDS

Abstract: A process for the preparation of ethylenically unsaturated compounds by contacting an acetylenically unsaturated compound or a 1,2-alkadiene with a Bronsted acid in the presence of a catalyst based on zero-valent ruthenium and a trivalent phosphorus containing compound.

Description: PROCESS FOR THE PREPARATION OF ETHYLENICALLY UNSATURATED COMPOUNDS The invention relates to a process for the preparation of ethylenically unsaturated compounds by reaction of an acetylenically unsaturated compound and/or an 1,2-alkadiene with a Bronsted acid in the presence of a ruthenium containing catalyst. The ruthenium-catalyzed addition of a Bronsted acid to the unsaturated bond of an acetylenically unsaturated compound is known. In Organometallics (1983), 2, pp. 1689-1691, by M. Rotem and Y. Shvo, the addition of carboxylic acids to alkynes, in particular internal alkynes such as diphenylacetylene, is disclosed. With the applied ruthenium-complexes, viz., [RU3 (CO) - j ^l and [Ru(CO)2 (CH3CO2) ] n , the reaction proceeds at low rate, whereby reaction times as long as 17 to 22 hours are recorded. According to these authors, a more simple catalyst such as RUCI3 is totally inactive. On the other hand, it is disclosed in Tetrahedron letters, Vol. 27, No. 52, pp. 6323-6324 (1986), by Chr. Ruppin and P.H. Dixneuf, that saturated and unsaturated carboxylic acids can be added to terminal alkynes, catalyzed by RUCI3.3H2O and RUCI2 (PMe 3 ) (p-cymene) . However, here again long reaction times (15 hours) were required and the reaction rate was low. The use of ruthenium(II) -containing catalysts, viz. bis (η^- cyclooctadienyl) ruthenium(II) (trialkylphosphine) (maleic anhydride), is disclosed by T. Mitsudo et al. in J. Org. Chem. (1987), 52, pp. 2230-2239. For the addition of unsaturated carboxylic acids, the presence of maleic acid in the catalyst system is not essential, but in the absence of maleic acid no reaction was observed with saturated carboxylic acids. Whereas the recorded reaction times are shorter (4 hours), the yields obtained show, that the reaction proceeds at relatively low catalyst turnover rate. According to EP-A-0,512, 656 a Bronsted acid may advantageously be added to an acetylenically unsaturated compound with the aid of a heterogeneous catalyst comprising ruthenium, preferably in the zero- valent state, supported on an inert porous support. The working examples are carried out with a ruthenium on carbon catalyst and with ethyne as the acetylenically unsaturated compound. It has now been found that very attractive results, in particular as regards the reaction rate, are obtained by using a catalyst based on a combination of zero-valent ruthenium and a ligand containing trivalent phosphorus. Moreover, this combination exhibits good catalytic activity for the addition of a Bronsted acid to an allenically unsaturated bond. The invention may be defined as relating to a process for the preparation of ethylenically unsaturated compounds by contacting an acetylenically unsaturated compound and/or an 1,2-alkadiene with a Bronsted acid in the presence of a catalyst based on zero-valent ruthenium and a trivalent phosphorus containing compound. The acetylenically unsaturated compounds which are suitable as starting material in the process of the invention include internal and terminal alkynes which may be unsubstituted or substituted with one or more substituents that do not interfere with the reaction with the Bronsted acid. The alkynes typically have from 2 to 10 carbon atoms. Examples of suitable substituents are alkoxy groups, typically with 1 to 4 carbon atoms, aryloxy groups and halogen atoms. Suitable internal acetylenes include butyne-2, pentyne-2, hexyne-2, hexyne-3, 1-phenylpropyne-l and diphenyl-acetylene. Preferably a terminal alkyne is used, for example ethyne, propyne, butyne-1 or phenylacetylene. Propyne represents a particularly preferred starting material. Commercially available propyne feedstocks usually comprise minor amounts of other unsaturated compounds, such as 1,2-propadiene. An advantage of the process of the invention consists in that the catalyst is also active in the reaction of an 1,2-alkadiene with a Bronsted acid. Consequently, if a commercial propyne feed is used that contains both propyne and 1,2-propadiene, the removal of the 1,2-alkadiene prior to the reaction involving the acetylenically unsaturated compound, can be omitted. In the present specification, a Bronsted acid is defined as a compound which can release one or more protons. Bronsted acids therefore include inorganic acids and organic acids, alcohols, amino compounds of sufficient acidity, hydroxy esters, amides and imides. Preferred Bronsted acids are carboxylic acids, both saturated and unsaturated carboxylic acids being suitable. Typical examples of suitable carboxylic acids are acetic acid, propionic acid, butyric acid, isobutyric acid, pivalic acid, acrylic acid, methacrylic acid, crotonic acid, benzoic acid, phthalic acid, isophthalic acid and terephthalic acid. Unsaturated carboxylic acids are most preferred. In particular methacrylic acid has proved to be a very attractive starting material. Examples of other suitable Bronsted acids include alcohols, such as methanol, ethanol, propanol-1 and propanol-2, phenol, hydroquinone and resorcinol, amino compounds, such as primary aliphatic amines and secondary aromatic amines, amides or imides, such as 2-pyrrolidone, succinimide and toluenesulphonamide. The source of zero-valent ruthenium is not critical. Metallic ruthenium may be used, conveniently in finely divided form and supported on a suitable carrier. If desired, a zero-valent ruthenium compound may be used, obtained by reduction of a ruthenium(II) , or a ruthenium(III)- compound. Preferably, a zero-valent ruthenium complex is used, such as complexes of ruthenium with cyano, carbon monoxide or ammonia groups. In particular preferred are complexes containing zero-valent ruthenium and carbon monoxide, such as [Ru(CO>5] and [RU3 (CO) 2] . The trivalent phosphorus compound participating in the catalysts of the invention, may be any phosphorus compound having a free electron pair at the phosphorus atom enabling the phosphorus compound to act as a ligand by complexing with ruthenium. Thus, suitable phosphorus compounds include phosphites, for example a mono-, or diphosphite, and phosphines. In the process of the invention phosphine ligands, in particular triarylphosphines such as triphenylphosphine, tritolylphosphine and trinaphthylphosphine, are preferred. Instead a compound acting as monodentate ligand, also compounds acting as bidentate ligands may be advantageously employed. Preferably, such compounds are represented by the general formula R 1 R 2 P-R-M-R 3 R 4 (I) wherein M represents a phosphorus or nitrogen atom, each of R---, R 2 , R 3 and R 4 independently represents a substituted or non-substituted hydrocarbyl group and R represents an organic bridging group containing from 1 to 4 atoms in the bridge. Preferably, M represents a phosphorus atom, in which case the compounds of formula (I) are bisphosphines. Each of R---, R 2 , R^ and 4 may represent a substituted or non- substituted aryl, alkaryl, aralkyl, alkyl, or cycloalkyl group. Also, R 1 together with R 2 and/or R 3 together with R 4 may form cyclic structures that are linked to the P and/or M atom. Each aryl, alkaryl or aralkyl group represented by R---, R 2 , R 3 or R 4 , typically has from 6 to 14, in particular from 6 to 10 carbon atoms. Aliphatic groups, represented by one or more of R 1 , R 2 , R 3 and R 4 , usually comprise from 1 to 8, in particular from 1 to 4 carbon atoms. Substituents may be conveniently selected from halogen atoms, cyano groups, alkoxy groups containing from 1 to 4 carbon atoms and hydroxy groups. In the compounds of formula (I) the bridging group, represented by R, preferably contains from 1 to 3 atoms in the bridge, usually all being carbon atoms. Most preferably, the bridging group consists of a single carbon atom. Typically the bridging group is a methylene group, but if one or both hydrogen atoms are replaced by substituents, R may also be a methanetriyl or methanetetrayl group. Examples of recommended compounds of formula (I) are bis (dialkylphosphino)alkanes, such as 1,2-bis (diethyl-phosphino)ethane, bis (di-n-butylphosphino)methane, 1,2-bis (diisobutylphosphino)ethane, 1,3- bis (diethylphosphino)propane, 1,3-bis (dimethylphosphino)propane and bis (di-sec.butylphosphino)methane, bis (diarylphosphino)alkanes, such as bis (diphenylphosphino)methane and bis (dinaphthylphosphino)methane, dialkylamino-diarylphosphinoalkanes, such as dimethylamino-diphenyl- phosphinomethane, diethylamino-diphenylphosphinomethane and 1,2- dimethylamino-diphenylphosphinoethane, and bis (cycloalkylenephosphino)alkanes, such as 1,2- bis (cyclooctylenephosphino)ethane, 1,3-bis (cyclooctylene- phosphino)propane, bis (cyclooctylenephosphino)methane and bis (cyclohexylenephosphino)methane. A special category of compounds acting as bidentate ligands is formed by compounds wherein the phosphorus atom is linked to a carbon atom of a nitrogen-containing aromatic group, for example a pyridyl group, pyridazinyl group or a pyrimidinyl group. The phosphorus atom may be linked to more than one or these groups, if so desired, or to one nitrogen-containing aromatic group and two other groups, such as phenyl groups. Examples of preferred ligands of this category are 2- diphenylphosphinopyridine, 2-diphenylphosphino-6-methylpyridine, 2- dimethylphosphinopyridine and 2-diphenylphosphinoquinoline. The amount of trivalent phosphorus containing compound is not critical. However, it is recommended to apply it in an amount of 0.5 to 20, preferably 1 to 5 moles per mole atom of ruthenium. The catalyst system used in the process of the invention, may be homogeneous or heterogeneous. If a heterogeneous catalyst is used, the zero-valent ruthenium and the trivalent phosphorus compound are supporte on an inert carrier. Suitable carrier materials include refractory oxides, such as alumina, silica, titania and silica-alumina and carbon. If supported, then supports, substantially consisting of carbon, are preferred. The Bronsted acid may usually constitute the reaction medium, so that no additional solvent or diluent is required. If desired, an additional diluent, such as aprotic liquids, may be used. Suitable examples are ethers, such as diethylether and 2,5,8-trioxanonane (diglyme) and ketones, such as methylethylketone and methylisobutylketone. The addition reaction is conveniently carried out at elevated temperatures, usually in the range of 50 - 200 °C. Preferred reaction temperatures are in the range of 80 - 160 °C. When acetylenically unsaturated compounds are used that are in the vapour state at the prevailing reaction temperature, the pressure is conveniently maintained in the range of 1 to 50 bar absolute. Usually, the partial pressure of the acetylenically unsaturated compound can be maintained below 10 bar, but for safety reasons, inert gases, such as nitrogen are often added. bringing the total pressure up to a value of say 25 bar. The products obtained by addition of a Bronsted acid to an unsaturated bond of the starting material may be linear or branched, depending, inter alia, on the selected catalyst combination. In particular, the non-linear addition products are of interest as intermediates in the preparation of speciality chemicals and as monomers in free radical initiated polymerization processes. It is believed that the selectivity with respect to a linear or non-linear addition product is affected by steric, as well as electronic factors involved in the coordination between the zero valent ruthenium and the specific phosphorus ligand. Thus, it has been observed that the use of a compound comprising a pyridyl group results in a high selectivity with respect to non-linear addition products. It will of course be appreciated that with acetylene as starting material, only linear addition products will be formed. The invention will be illustrated by the following non-limiting examples. Example 1 After being flushed, a 250 mL autoclave was charged with 30 mL of methacrylic acid, 50 mL of 2,5, 8-trioxanonane, 2 bar of propyne, 106 mg of a zero valent ruthenium-carbon monoxide complex [RU3 (CO) ^2. a d 260 m of triphenylphosphine. For safety reasons 20 bar of nitrogen was added. Upon sealing, the contents of the autoclave were heated to 130 °C for 5 hours. Subsequently the autoclave was cooled to ambient temperature and the contents were analyzed by means of gas-liquid chromatography. It was found that 35% of the propyne had been converted and that the selectivit to isopropenylacrylate was 91%. The reaction rate was calculated to be 42 mol product per mole atom of ruthenium and per hour. The catalyst composition, reaction time, selectivity to the isoalkenylester and reaction rate are shown in Table 1. Examples 2-15 A number of experiments were carried out, substantially as described in Example 1, but using other phosphorus compounds, instead of triphenylphosphine. The catalyst composition, reaction time, selectivity to the isoalkenylester and reaction rate are shown in Table 1. Example A (for comparison, not according to the invention) An experiment was carried out, substantially as described in Exampl 1, with the difference that instead of triphenylphosphine, bis (dimethylamino)ethane was used as catalyst component. The catalyst composition, reaction time, selectivity to the isoalkenylester and reaction rate are shown in Table 1. From the results it can be seen that by using a catalyst ligand which does not contain trivalent phosphorus, the selectivity to the isoalkenylester was only 54% and that the reaction proceeded at a very low rate. Examples 16-19 A number of experiments were carried out, substantially as describe in Example 12, but using another Bronsted acid, instead of methacrylic acid and (as regards Examples 18 and 19) another unsaturated starting material, instead of propyne. The reactants, reaction time, selectivity to the isoalkenyl ester and reaction rate are shown in Table 2. Table 1 Example Catalyst composition Reaction Selectivity Rate No. [Ru 3 ( CO ) 12 ] Ligand (mmol) time (hr) isoalkenyl¬ (mol/mol-hr) (mmol Ru) ester (%) 1 0.5 triphenylphosphine 1 5 91 42 2 0.5 trinaphthylphosphine 1 10 39 44 3 0.5 bis (diphenylphosphino)methane 0.5 5 89 122 4 0.5 1,2-bis (diisobutylphosphino)ethane 0.5 10 63 57 5 0.5 1,2-bis (diethylphosphino)ethane 0.5 10 68 60 6 0.5 1,3-bis (diethylphosphino)propane 0.5 10 65 60 7 0.5 1,3-bis (dimethylphosphino)propane 0.5 10 59 60 8 0.5 1,3-bis (cyclooctylenephosphino)propane 0.5 10 65 48 00 9 0.5 1,2-bis (cyclooctylenephosphino)ethane 0.5 10 69 42 I 10 0.5 bis (cyclooctylenephosphino)methane 0.5 10 81 57 11 0.5 dimethylamino-diphenylphosphinomethane 0.5 5 91 119 A 0.5 bis (dimethylamino)ethane 0.5 5 54 9 12 0.5 2-diphenylphosphinopyridine 0.5 3 90 234 13 0.5 2-diphenylphosphinoquinoline 0.5 3 90 195 14 0.5 2-dimethylphosphinopyridine 0.5 2 84 228 15 0.5 2-diphenylphosphino-6-methylpyridine 0.5 4 90 150 Table 2 Example Unsaturated Bronsted acid (mL) Reaction time Selectivity Rate No. starting material (hr) isoalkenylester (mol/mol'hr) (bar) (%) 16 propyne 2 acetic acid 30 0.75 79 200 17 propyne 2 pivalic acid 30 5 88 133 18 allene 5 pivalic acid 30 10 75 20 19 ethyne 1.6 pivalic acid 30 5 (100) 75

Claims: C A I M S 1. A process for the preparation of ethylenically unsaturated compounds by contacting an acetylenically unsaturated compound and/or an 1,2-alkadiene with a Bronsted acid in the presence of a catalyst based on zero-valent ruthenium and a trivalent phosphorus containing compound. 2. A process as claimed in claim 1, wherein propyne is used. 3. Process as claimed in claim 1 or 2, wherein as Bronsted acid a carboxylic acid, preferably an unsaturated carboxylic acid is used. 4. A process as claimed in claim 3, wherein methacrylic acid is used. 5. A process as claimed in any one of claims 1 to 4, wherein as catalyst a complex is used, containing zero-valent ruthenium, carbon monoxide and a trivalent phosphorus containing compound acting as ligand. 6. A process as claimed in any of claims 1-5, wherein the trivalent phosphorus containing compound is a phosphine. 7. A process as claimed in any of claims 1-6, wherein the catalyst comprises a compound acting as a bidentate ligand. 8. A process as claimed in claim 7, wherein as bidentate ligand a compound is used having the general formula R 1 R 2 P-R-M-R 3 R 4 (I) wherein M represents a phosphorus or nitrogen atom, each of R 1 , 2 , R? and R 4 independently represents a substituted or non-substituted hydrocarbyl group and R represents an organic bridging group containing from 1 to 4 atoms in the bridge. 9. A process as claimed in claim 8, wherein in the compound of formula (I), M represents a phosphorus atom. 10. A process as claimed in claim 9, wherein in the compound of formula (I), R represents a bridging group containing 1 carbon atom in the bridge. 11. A process as claimed in claim 7, wherein in the compound the phosphorus atom is linked to a 2-pyridyl group. 12. A process as claimed in claim 11, wherein the compound is 2- diphenylphosphinopyridine or 2-dimethylphosphinopyridine.

Inventors: DRENT EIT, JAGER WILLEM WABE, DRENT, EIT, JAGER, WILLEM, WABE
Applicants: SHELL INT RESEARCH, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1994
Main classification: C07C67
IPC codes: B01J31, C07B61, C07C5, C07C11, C07C67